US4897267A - Microparticles comprising a biodegradable polymer controlling the release of an antimalaria active principle, pharmaceutical compositions comprising it and process for its preparation - Google Patents
Microparticles comprising a biodegradable polymer controlling the release of an antimalaria active principle, pharmaceutical compositions comprising it and process for its preparation Download PDFInfo
- Publication number
- US4897267A US4897267A US07/225,395 US22539588A US4897267A US 4897267 A US4897267 A US 4897267A US 22539588 A US22539588 A US 22539588A US 4897267 A US4897267 A US 4897267A
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- United States
- Prior art keywords
- microparticles
- polymer
- active principle
- weight
- primaquine
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- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P33/00—Antiparasitic agents
- A61P33/02—Antiprotozoals, e.g. for leishmaniasis, trichomoniasis, toxoplasmosis
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/30—Against vector-borne diseases, e.g. mosquito-borne, fly-borne, tick-borne or waterborne diseases whose impact is exacerbated by climate change
Definitions
- the present invention relates to the incorporation of antimalaria agents in polymeric biomaterials by microencapsulation.
- Microencapsulation groups all of the techniques enabling the obtaining of individualized particles whose size ranges between 1 and 1250 ⁇ m.
- microparticles so obtained may be divided into two groups:
- microcapsules spherical particles constituted by a solid jacket containing a liquid, solid or pasty substance.
- Each microcapsule constitutes a reservoir system proper;
- This structure homogeneous or heterogeneous as the case may be, constitute a matrix system.
- Antimalarial agents concerned by the present invention have been described in patent applications FR 87 04079 and BE 200041. They are primaquine and its derivatives such as amino acid-primaquine derivatives, targeted macromolecular conjugates, such as primaquine bonded to galactosylated albumin through a tetrapeptide arm which permits the release of an active form of primaquine at the level of the lysosomes of the targeted cells. These antimalarial agents seek to combat the hepatocyte forms of malaria.
- a difficulty of the inventions in the field which interests us is the need to determine the polymers having properties defined according to the type of active principle to be incorporated. It is appropriate also to determine for a given drug type the speed of release and the charge ratio ensuring optimum therapeutic coverage for a selected period.
- the technique of incorporation depends on the polymer-medicament couple particularly the existence of a solvent common to the partners, the existence of thermal properties of the latter, their miscibility, etc. In addition, this incorporation must not alter the properties of the active principle.
- One of the objects of the present invention is therefore the production of injectable microparticulate forms enabling the release kinetics to be modulated by means of polymeric materials for a series of molecules active against malaria.
- Medicaments absorbed orally may be coated by a non-biodegradable filmogenic polymer, since it will be eliminated through the tractus after being released at the level of the stomach or at the entry of the intestine.
- the polymers must show particular properties, especially of biodegradability.
- microparticles containing a principle active against malaria such as primaquine, one of its derivatives or their conjugates with a hepatotropic vector or their pharmaceutically acceptable salts, and a biocompatible and biodegradable polymer controlling the release kinetics of the active principle.
- PQ represents primaquine
- X represents an amino acid or a peptide of 2 to 4 amino acids
- linkage PQ--X being a covalent peptide linkage between the free amine group of PQ and the carboxylic group of X.
- the basic products PQ as well as derivatives such as PQ--X may be in the form of their addition salts with acids.
- a start is made from a salt, for example, the diphosphate of primaquine and the amino acid or peptide whose amino function is protected, for example, by a terbutyloxycarbonyl group and the following steps are carried out.
- a salt for example, the diphosphate of primaquine and the amino acid or peptide whose amino function is protected, for example, by a terbutyloxycarbonyl group and the following steps are carried out.
- N-hydroxysuccinimide or any other group activating the acid function of the amino acid or peptide is reacted with the protected derivative of the amino acid or peptide, for example, on the N-terbutyloxycarbonyl derivative of the amino acid or peptide,
- the protective group such as the terbutyloxycarbonyl of the compound obtained is then cleaved in the presence of acid, for example trifluoroacetic acid to give the derivative PQ-X in salt form, for example, trifluoroacetate.
- the primaquine acts as an oxidizing agent and destabilizes the membrane of the red blood cells causing hemolysis which is at the origin of its principal toxicity.
- amino acids may be mentioned particularly L-leucine, D-leucine, L-alanine, D-alanine, L-isoleucine, L-phenylalanine, L-glutamic acid, L-lysine, L-tyrosine and L-glutamine.
- the dipeptides L-alanyl-L-leucyl, L-leucyl-L-alanyl may be mentioned the dipeptides L-alanyl-L-leucyl, L-leucyl-L-alanyl, but also the tetrapeptides (L-analyl-L-leucyl) 2 , (L-alanyl) 3 L-leucyl, L-alanyl-L-leucylglycyl-L-leucyl, glycyl-L-leucyl-glycyl-L-leucyl.
- the conjugates with a hepatotropic vector may be, for example, targeted macromolecular conjugates of primaquine bonded to galactosylated albumin through a tetrapeptide arm described in BE 200041, but advantageously the hepatotropic vector will have a low molecular weight and will be synthetic.
- microparticles according to the invention are microspheres constituted by a matrix of polymers within which the antimalarial active principle is distributed.
- the polymer is polylactide.
- the polyactide polymers are characterized by a biodegradability whose degradation kinetics are particularly convenient to control the release of primaquine and its derivatives.
- polyglycolides for example, although also biodegradable, show a too rapid speed of biodegradation for this type of active principle and polycaprolactones show a too slow speed of degradation for the type of use envisaged for the present invention.
- Polylactide is preferably in (DL) form.
- the molecular weight of the polymer is advantageously comprised between 10,000 and 200,000, preferably between 50,000 and 100,000.
- the ratio by weight of active principle/polymer is advantageously comprised between 1 and 50% and preferably between 15 and 25%.
- the microparticles are formulated in an injectable solution.
- the microparticles must have a size comprised between 1 and 250 ⁇ m, preferably comprised between 100 and 200 ⁇ m.
- a polymer is dissolved in a volatile solvent
- this phase is then emulsified in a dispersing non-miscible medium
- microparticles are recovered by centrifugation and filtration.
- the primaquine and its derivatives being water soluble, in a particular embodiment of the process according to the invention, the primaquine or one of its pharmaceutically acceptable salts is incorporated in polyactide, the solvent being acetone, the dispersant non-miscible medium being a mineral oil, such as paraffin, the substance regulating the size of the particles being a non-ionic surface-active agent.
- the (DL) form of the polyactide which is most soluble in acetone is very suitable for this type of process.
- the ratio by weight polymer/solvent is advantageously from 10 to 30%, preferably from 15 to 20%.
- the emulsification is done with vigorous stirring. In this way, it is possible to obtain microparticles of size less than 200 ⁇ m such as preferred to render these microparticles injectable.
- sorbitan esters particularly sorbitan monooleate, in a concentration comprised between 1 and 10% with respect to the weight of the solvent.
- Tables 1 to 4 show the particle size distribution of microspheres prepared according to the invention, the in vitro release kinetics of microspheres of diameter comprised between 160 and 200 ⁇ m, and the therapeutic activity of the latter.
- the amount of surface-active agent must be comprised between 1 and 10% with respect to the weight of the acetone and preferably 5% with span 80.
- Tests were carried out by using different surface active agents at different concentrations.
- the surface-active agents used were the following: aluminum tristearate, and various sorbitan esters and particularly:
- HLB hydrophile-lipophile balance of their molecules
- microspheres of smallest average size are obtained with 5% span 80.
- particles of smaller sizes are obtained with other sorbitan esters than with aluminum tristearate.
- the conditions of emulsification are also extremely critical. Subjecting the system to mechanical stirring of 800 rpm during the addition, the average size of the microspheres is considerably reduced. In this way it is possible to obtain a considerable proportion of microspheres of size less than 200 ⁇ m (Table 1). For the in vitro and in vivo studies, the granulometric fraction comprised between 160 and 200 ⁇ m was used.
- the loading ratio ie. the ratio of incorporation of primaquine in the microspheres, is proportional to the size of the microspheres.
- loading ratios of active principle of the order of 15% are obtained.
- the "loading ratio” is signified by L.R.: (weight of active principle)/(weight of microspheres).
- the suspending of the primaquine phosphate in the acetone solution of polymer is not easy, the active principle agglomerating in the form of lumps difficult to disperse. It is important to use the active principle in finest granulometric form. Satisfactory results have been obtained by the dispersion of the powder with ultrasound, at the power of 100 watts for some minutes.
- the preventive activity of the primaquine thus incorporated was determined in the experimental model of murine malaria (Plasmodium berghei, ANKA strain, female OFl swiss mice).
- the microspheres of granulometric size comprised between 160 and 200 ⁇ m were administered intramuscularly, 3 to 17 days before the infection of the mice with P. berghei sporozoites.
- the microsphere preparations of (DL) polyactide containing primaquine had a smaller burst effect and regular release comprised between 9 and 14 days.
- the therapeutic programme (injected doses, periods of coverage) was selected on the basis of daily average release characteristic of each of the preparations ST11 (8% of Pq), ST12 (11.1% of Pq) and ST17 (7.7% of Pq).
- the daily concentration of Pq necessary to obtain complete protection of the infected animals is about 50 mg Pq/kg although the release in the animal is similar to the in vitro release.
- the optimal period of coverage is, in the model of murine malaria, 14 days.
- the partial protection is obtained at the dosage of 450 mg Pq/mg namely 36 mg/kg/day and complete protection of the infected animals at the dose of 625 mg Pq/kg namely 50 mg Pq/kg/day.
- the dose of 700 mg Pq/kg (50 mg Pq/kg/day) is completely curative at 14 days but is no more than partly active at 17 days.
- the aminoacylated derivatives of primaquine are obtained in two steps starting from primaquine diphosphate and from the amino acid whose amino function is protected by an N-terbutyloxycarbonyl (N-TBoc) group.
- the first step comprises the reaction of the primaquine base with the N-hydroxysuccinimide ester o the N-TBoc derivative of the amino acid.
- the TBoc is then cleaved in the presence of trifluoroacetic acid.
- the aminoacylated derivative of primaquine is obtained in the form of trifluoroacetate (probably a ditrifluoroacetate salt).
- the aminoacylated derivative of primaquine in its free base form may be obtained by neutralising the aqueous solution containing the trifluoroacetate salt of aminoacyl-Pq with NH 4 OH up to pH ⁇ 8 followed by vigorous extraction with dichloromethane. After evaporation of the CH 2 Cl 2 , there is obtained a greenish oil very difficult to handle which may be purified subsequently by chromatography on a silicagel column eluted with a mixture CH 2 Cl 2 --EtOH--NH 4 OH (120-20-1).
- the column used is a Merck lobar 8 column.
- the support is a silica bonded with C 8 residues.
- elution solvents are carefully degasified.
- the crude product dissolved in an aqueous acid medium is adsorbed at the head of the column; there then follows a desalting step (H 2 O--H + ) before eluting the product by using a CH 3 CN gradient in H 2 O/H+.
- the eluant is fractionated.
- the fractions containing the product are analysed by HPLC. Those containing the product with a purity higher than 98% are collected and freeze-dried. A bright orange-yellow powder is obtained.
- the trifluoroacetate counter anion is then changed into a hydrochloride by adding to an aqueous solution of the trifluoroacetate salt an amount of aqueous HCl corresponding approximately to two acid equivalents calculated with respect to the weight of trifluoroacetate salt to be exchanged.
- the solution obtained (pH 2.8-3) is freeze-dried protected from light (two lyophilisations).
- the product obtained is in the form of a very hygroscopic bright orange powder. Even stocked under an inert atmosphere (argon), the product deteriorates fairly rapidly in the course of time. It also shows a limited stability in solution: physiological medium or aqueous solution at 0° C. and protected from light.
- the quinoleic nucleus is a particularly sensitive target for any oxidation reaction. The latter explains partly the instability observed.
- the aqueous solution containing the trifluoroacetate salt was treated with sodium bisulfite (0.1%).
- the relative proportion CH 3 CN--H 2 O/H + varies according to the nature and the number of amino acids bonded to the primaquine.
- the organic phase was dried on sodium sulfate, filtered and evaporated.
- the product was purified on silicagel using as eluants a dichloromethane-methanol mixture. The pure fractions were collected and the eluant evaporated resulting in 1.5 g of a more or less crystalline product which was fairly hygroscopic.
- the product obtained previously was dissolved in 15 ml of a 1:1 mixtureof dichloromethane and trifluoroacetic acid. The mixture was stirred for 30 minutes at room temperature. The solvents were evaporated under vacuum and the residue was taken up again in water and washed several times with diisopropylether.
- the product was purified by reverse phase chromatography (Merck lobar 8) by using as an eluant a mixture of 25% of acetonitrile in water containing 1% of trifluoroacetic acid.
- the pure fractions (HPLC) were collected, the acetonitrile driven off under vacuum. After 2 lyophilisation cycles, 1.6 g (80%) of a hygroscopic bright orange powder was obtained.
- microspheres were prepared by the operational method presented in Example 1.
- the granulometric distribution of 3 preparations is shown in Table 4.
- primaquine diphosphate a large proportion of injectable microspheres was obtained.
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Abstract
Description
TABLE 1
______________________________________
Granulometric distribution (%) of four (DL)
polylactide microspheres preparations containing
primaquine diphosphate.
Diameter of the microparticles (μm)
Sample
70-100 100-160 160-200
200-250 250-315
>315
______________________________________
ST 11 0.1 5.1 17.9 50.0 23.6 3.3
ST 12 3.3 45.1 39.8 10.0 1.4 0.2
ST 71 0.3 7.5 24.0 47.8 18.6 1.8
ST 81 1.2 43.1 41.8 11.0 2.1 0.7
______________________________________
TABLE 2
______________________________________
Load ratio and kinetics of release in vitro
of the granulometric fractions 160-200 μm.
Average
Amount released
release
Loading after 1 hour speed
Sample ratio (%) (%) (% day)
______________________________________
ST 11 15.0 0 8.0
ST 12 14.5 0 11.1
ST 71 16.1 4.2 7.7
ST 81 17.9 4.8 8.6
______________________________________
TABLE 3
______________________________________
Preventive prophylactic activity of
primaquine diphosphate incorporated in (DL)
polylactide microspheres.
Loading Treat-
ratio Dose.sup.a
ment.sup.b LTS.sup.c
Specimen (%) (mg/kg) (days) LTS/N (%)
______________________________________
ST 11 15 450 -7 3/5 60
625 -7 5/5 100
ST 12 14.5 450 -3 5/5 100
450 -7 5/5 100
ST 71 16.1 700 -10 5/5 100
700 -14 5/5 100
700 -17 3/5 60
______________________________________
.sup.a The microspheres of granulometric size comprised between 160 and
200 μm are injected in 812 miglyol solution (viscosified with 4%
Thixcin R) intramuscularly. The concentrations are expressed in mg of
primaquine diphosphate/kg.
.sup.b The treated animals are infected with P. berghei sporazoites, 3 to
17 days after the treatment.
.sup.c Preventive prophylactic activity (%) = the number of animals
protected to the number of animals treated and infected (expressed as %).
TABLE 4
______________________________________
Granulometric distribution (%) of three
preparations of (DL) polylactide microspheres
containing L-glutamyl primaquine.
Diameter of the microparticles (μm)
Sample 70-100 100-160 160-200
200-250 250-315
>315
______________________________________
PH 52A 1.1 14.8 31.9 43.2 8.4
0.5
PH 52B 1.3 18.8 19.8 20.6 28.9
10.6
PH 52C 0.5 5.7 16.4 49.6 26.4
1.3
______________________________________
Claims (20)
PQ--X
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR8710802A FR2618674B1 (en) | 1987-07-30 | 1987-07-30 | MICROPARTICLES COMPRISING A BIODEGRADABLE POLYMER CONTROLLING THE RELEASE OF AN ANTIMALARIA ACTIVE INGREDIENT, PHARMACEUTICAL COMPOSITIONS COMPRISING SAME AND METHOD OF PREPARATION |
| FR8710802 | 1987-07-30 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4897267A true US4897267A (en) | 1990-01-30 |
Family
ID=9353715
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/225,395 Expired - Fee Related US4897267A (en) | 1987-07-30 | 1988-07-28 | Microparticles comprising a biodegradable polymer controlling the release of an antimalaria active principle, pharmaceutical compositions comprising it and process for its preparation |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US4897267A (en) |
| EP (1) | EP0301969B1 (en) |
| JP (1) | JPS6442433A (en) |
| AT (1) | ATE66372T1 (en) |
| CA (1) | CA1329549C (en) |
| DE (1) | DE3864348D1 (en) |
| ES (1) | ES2024668B3 (en) |
| FR (1) | FR2618674B1 (en) |
| GR (1) | GR3002601T3 (en) |
Cited By (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5110935A (en) * | 1988-09-23 | 1992-05-05 | Ire-Celltarg, S.A. | New compounds which are active against the tissue forms of malaria and method of preparation |
| US5292512A (en) * | 1988-12-20 | 1994-03-08 | Centre Internationale De Recherches Dermatologiques (C.I.R.D.) | Cosmetic or pharmaceutical composition containing microspheres of polymers or of fatty substances filled with at least one active product |
| US5389379A (en) * | 1992-02-18 | 1995-02-14 | Akzo N.V. | Process for the preparation of biologically active material containing polymeric microcapsules |
| US5417982A (en) * | 1994-02-17 | 1995-05-23 | Modi; Pankaj | Controlled release of drugs or hormones in biodegradable polymer microspheres |
| US5514378A (en) * | 1993-02-01 | 1996-05-07 | Massachusetts Institute Of Technology | Biocompatible polymer membranes and methods of preparation of three dimensional membrane structures |
| US5569468A (en) * | 1994-02-17 | 1996-10-29 | Modi; Pankaj | Vaccine delivery system for immunization, using biodegradable polymer microspheres |
| WO1996040068A1 (en) * | 1995-06-07 | 1996-12-19 | Inhale Therapeutic Systems | Methods and system for processing dispersible fine powders |
| US5766635A (en) * | 1991-06-28 | 1998-06-16 | Rhone-Poulenc Rorer S.A. | Process for preparing nanoparticles |
| US5981719A (en) | 1993-03-09 | 1999-11-09 | Epic Therapeutics, Inc. | Macromolecular microparticles and methods of production and use |
| US6090925A (en) | 1993-03-09 | 2000-07-18 | Epic Therapeutics, Inc. | Macromolecular microparticles and methods of production and use |
| US6203802B1 (en) | 1990-03-16 | 2001-03-20 | L'oreal | Composition for the cosmetic and/or pharmaceutical treatment of the upper layers of the epidermis by topical application to the skin, and corresponding preparation process |
| USRE37410E1 (en) | 1994-08-02 | 2001-10-16 | Massachusetts Institute Of Technology | Controlled local delivery of chemotherapeutic agents for treating solid tumors |
| US6306425B1 (en) | 1999-04-09 | 2001-10-23 | Southern Research Institute | Injectable naltrexone microsphere compositions and their use in reducing consumption of heroin and alcohol |
| US6495155B1 (en) | 1999-08-27 | 2002-12-17 | Southern Research Institute | Injectable opioid partial agonist or opioid antagonist microparticle compositions and their use in reducing consumption of abused substances |
| US6689608B1 (en) | 1993-02-01 | 2004-02-10 | Massachusetts Institute Of Technology | Porous biodegradable polymeric materials for cell transplantation |
| US6716251B1 (en) | 1997-06-13 | 2004-04-06 | Aventis Pharmaceuticals Holdings, Inc. | Implant for subcutaneous or intradermal injection |
| US20050106120A1 (en) * | 2001-11-12 | 2005-05-19 | Shujun Cheng | Polyester containing active drugs and having amino acids in the main chain & comma; and its preparation method |
| US20060141000A1 (en) * | 1993-02-01 | 2006-06-29 | Mikos Antonios G | Porous biodegradable polymeric materials for cell transplantation |
| US20080241251A1 (en) * | 2004-01-21 | 2008-10-02 | Abdul Waseh Basit | Method of Producing Microparticles |
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- 1987-07-30 FR FR8710802A patent/FR2618674B1/en not_active Expired - Fee Related
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- 1988-07-28 US US07/225,395 patent/US4897267A/en not_active Expired - Fee Related
- 1988-07-28 ES ES88401965T patent/ES2024668B3/en not_active Expired - Lifetime
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Cited By (29)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5110935A (en) * | 1988-09-23 | 1992-05-05 | Ire-Celltarg, S.A. | New compounds which are active against the tissue forms of malaria and method of preparation |
| US5292512A (en) * | 1988-12-20 | 1994-03-08 | Centre Internationale De Recherches Dermatologiques (C.I.R.D.) | Cosmetic or pharmaceutical composition containing microspheres of polymers or of fatty substances filled with at least one active product |
| US6203802B1 (en) | 1990-03-16 | 2001-03-20 | L'oreal | Composition for the cosmetic and/or pharmaceutical treatment of the upper layers of the epidermis by topical application to the skin, and corresponding preparation process |
| US5766635A (en) * | 1991-06-28 | 1998-06-16 | Rhone-Poulenc Rorer S.A. | Process for preparing nanoparticles |
| US5389379A (en) * | 1992-02-18 | 1995-02-14 | Akzo N.V. | Process for the preparation of biologically active material containing polymeric microcapsules |
| US5514378A (en) * | 1993-02-01 | 1996-05-07 | Massachusetts Institute Of Technology | Biocompatible polymer membranes and methods of preparation of three dimensional membrane structures |
| US8110213B2 (en) | 1993-02-01 | 2012-02-07 | Massachusetts Institute Of Technology | Method of forming a tissue structure by introducing cells into an implanted matrix |
| US6689608B1 (en) | 1993-02-01 | 2004-02-10 | Massachusetts Institute Of Technology | Porous biodegradable polymeric materials for cell transplantation |
| US7462471B2 (en) | 1993-02-01 | 2008-12-09 | Massachusetts Institute Of Technology | Porous biodegradable polymeric materials for cell transplantation |
| US20060141000A1 (en) * | 1993-02-01 | 2006-06-29 | Mikos Antonios G | Porous biodegradable polymeric materials for cell transplantation |
| US5981719A (en) | 1993-03-09 | 1999-11-09 | Epic Therapeutics, Inc. | Macromolecular microparticles and methods of production and use |
| US6090925A (en) | 1993-03-09 | 2000-07-18 | Epic Therapeutics, Inc. | Macromolecular microparticles and methods of production and use |
| US6268053B1 (en) | 1993-03-09 | 2001-07-31 | Epic Therapeutics, Inc. | Macromolecular microparticles and methods of production and use |
| US5569468A (en) * | 1994-02-17 | 1996-10-29 | Modi; Pankaj | Vaccine delivery system for immunization, using biodegradable polymer microspheres |
| US5417982A (en) * | 1994-02-17 | 1995-05-23 | Modi; Pankaj | Controlled release of drugs or hormones in biodegradable polymer microspheres |
| USRE37410E1 (en) | 1994-08-02 | 2001-10-16 | Massachusetts Institute Of Technology | Controlled local delivery of chemotherapeutic agents for treating solid tumors |
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| US6716251B1 (en) | 1997-06-13 | 2004-04-06 | Aventis Pharmaceuticals Holdings, Inc. | Implant for subcutaneous or intradermal injection |
| US20040191323A1 (en) * | 1997-06-13 | 2004-09-30 | Aventis Pharmaceuticals Holdings, Inc. | Implant for subcutaneous or intradermal injection |
| US20100221684A1 (en) * | 1997-06-13 | 2010-09-02 | Aventis Pharmaceuticals | Implant for subcutaneous or intradermal injection |
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| US6495155B1 (en) | 1999-08-27 | 2002-12-17 | Southern Research Institute | Injectable opioid partial agonist or opioid antagonist microparticle compositions and their use in reducing consumption of abused substances |
| US20050106120A1 (en) * | 2001-11-12 | 2005-05-19 | Shujun Cheng | Polyester containing active drugs and having amino acids in the main chain & comma; and its preparation method |
| US20080241251A1 (en) * | 2004-01-21 | 2008-10-02 | Abdul Waseh Basit | Method of Producing Microparticles |
| US8343545B2 (en) * | 2004-01-21 | 2013-01-01 | University College London | Method of producing microparticles |
Also Published As
| Publication number | Publication date |
|---|---|
| FR2618674A1 (en) | 1989-02-03 |
| ES2024668B3 (en) | 1992-03-01 |
| CA1329549C (en) | 1994-05-17 |
| EP0301969B1 (en) | 1991-08-21 |
| FR2618674B1 (en) | 1990-06-15 |
| GR3002601T3 (en) | 1993-01-25 |
| DE3864348D1 (en) | 1991-09-26 |
| JPS6442433A (en) | 1989-02-14 |
| EP0301969A1 (en) | 1989-02-01 |
| ATE66372T1 (en) | 1991-09-15 |
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